KR102358506B1 - Processing Method For Nylon Upcycle - Google Patents

Processing Method For Nylon Upcycle Download PDF

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KR102358506B1
KR102358506B1 KR1020210019191A KR20210019191A KR102358506B1 KR 102358506 B1 KR102358506 B1 KR 102358506B1 KR 1020210019191 A KR1020210019191 A KR 1020210019191A KR 20210019191 A KR20210019191 A KR 20210019191A KR 102358506 B1 KR102358506 B1 KR 102358506B1
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nylon
bulk
waste material
sample
viscosity
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KR1020210019191A
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Korean (ko)
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이승우
오대헌
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영남대학교 산학협력단
(주)에스디지엔텍
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/007Treatment of sinter powders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/02Conditioning or physical treatment of the material to be shaped by heating
    • B29B13/022Melting the material to be shaped
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • C08J11/06Recovery or working-up of waste materials of polymers without chemical reactions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0255Specific separating techniques using different melting or softening temperatures of the materials to be separated
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0424Specific disintegrating techniques; devices therefor
    • B29B2017/0496Pyrolysing the materials
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

The present invention relates to a nylon upcycle processing method capable of recovering a nylon resin and a nylon fiber product, which are discarded, efficiently removing impurities, classifying the nylon resin and the nylon fiber product for each physical property, and reprocessing the nylon resin and the nylon fiber product into recycled nylon raw materials having a specific color and a specific physical property. The nylon upcycle processing method includes: a first step of selecting a specific nylon from a nylon waste material bulk that has been received; a second step of testing a viscosity by melting a sample of the selected nylon waste material bulk; a third step of classifying the nylon waste material bulk according to the viscosity and a color; a fourth step of selectively blending a plurality of nylon waste material bulks according to a desired viscosity and a desired color; and a fifth step of producing a recycled nylon raw material by mixing an additive with the blended nylon waste material bulks, and melting and processing a mixture.

Description

나일론 업싸이클 가공방법{Processing Method For Nylon Upcycle}Nylon Upcycle Processing Method {Processing Method For Nylon Upcycle}

본 발명은 나일론 업싸이클 가공방법에 관한 것으로, 보다 상세하게는 폐기되는 나일론 수지 및 나일론 섬유 제품을 회수하여 효율적으로 불순물을 제거하고 물성 별로 분류한 후 특정한 색상과 물성을 보유한 나일론 재생 원료로 재가공하는 나일론 업싸이클 가공방법에 관한 것이다.The present invention relates to a nylon upcycle processing method, and more particularly, it is a method of recovering discarded nylon resin and nylon fiber products, efficiently removing impurities, classifying them by physical properties, and reprocessing them as nylon recycled raw materials with specific colors and properties. It relates to a nylon upcycle processing method.

산업의 발달 또는 생활의 편리함 등을 이유로 현재 합성수지 또는 합성섬유 제품이 많이 사용되고 있으며, 이에 따라 합성수지 또는 합성섬유 폐기물 또한 심각하게 발생되고 있다. 합성수지 또는 합성섬유 폐기물을 처리하는 방법으로 소각하거나 매립하는 방법이 있으나, 소각에 의한 처리는 소각시 유해가스를 다량으로 방출하여 인근 지역의 대기를 오염시키는 문제가 있어 기피되고 있다. 또한, 매립에 의한 처리는 매립지를 구하기가 힘들 뿐만 아니라, 합성수지 또는 합성섬유의 특성상 그 분해 속도가 매우 느리고 침출수에 의한 매립지 오염 문제가 있어 역시 기피되고 있는 방법이다.Due to industrial development or convenience of life, synthetic resin or synthetic fiber products are currently widely used, and accordingly, synthetic resin or synthetic fiber waste is also seriously generated. There is a method of incineration or landfill as a method of treating synthetic resin or synthetic fiber waste, but treatment by incineration is avoided because it emits a large amount of harmful gas during incineration and pollutes the atmosphere of the surrounding area. In addition, the treatment by landfill is not only difficult to obtain a landfill, but also has a very slow decomposition rate due to the characteristics of synthetic resins or synthetic fibers, and there is a problem of contamination of the landfill by leachate.

이에 합성수지 또는 합성섬유 폐기물에 대한 재활용의 필요성이 매우 높아지고 있으나, 아래와 같은 문제점을 내포하고 있다.Accordingly, the need for recycling of synthetic resin or synthetic fiber waste is increasing, but it has the following problems.

첫째, 합성수지 또는 합성섬유 폐기물의 회수와 선별에 많은 설비와 인원이 투입되어야 한다. 회수되는 합성수지 또는 합성섬유 폐기물에는 불순물이 섞여 있는 경우가 대부분이므로 재활용 제품의 품질을 확보하기 위해서는 회수된 폐기물의 선별에 많은 설비와 인원이 필요하게 되어 비용이 높아질 수밖에 없는 문제가 있다. 둘째, 재활용 제품의 품질에 대한 문제이다. 합성수지 또는 합성섬유의 폐기물 회수와 선별에 막대한 설비와 인원을 투입하더라도 재활용되는 원료의 순도가 부족하여 신규 원료와 혼용하여 사용되거나 저급 원료로 사용되고 있다.First, a lot of equipment and personnel must be put into the collection and sorting of synthetic resin or synthetic fiber waste. Since most of the recovered synthetic resin or synthetic fiber waste contains impurities, in order to secure the quality of recycled products, many facilities and personnel are required to sort the recovered waste, which inevitably increases the cost. Second, it is a matter of the quality of recycled products. Even if enormous facilities and personnel are put into waste collection and sorting of synthetic resins or synthetic fibers, the purity of the recycled raw materials is insufficient, so they are used in combination with new raw materials or are used as low-grade raw materials.

현재 각종 산업 분야에서 많이 사용되고 있는 나일론 섬유 또는 나일론 수지 또한 재활용이 가능한 소재이지만, 이러한 문제로 인하여 재활용에 어려움이 있다. 특히, 나일론 수지 제품의 경우 유리 섬유나 다른 합성수지와 혼합되어 사용되는 경우가 많아 완제품을 해체하거나 불순물을 선별하는 작업이 반드시 선행되어야 하고, 나일론 6과 나일론 66은 물성이 전혀 상이하여 나일론 섬유 또는 나일론 수지 폐기물을 원재료에 따라 부가적으로 선별해 주어야 한다.Nylon fiber or nylon resin, which is currently widely used in various industrial fields, is also a recyclable material, but it is difficult to recycle due to this problem. In particular, nylon resin products are often mixed with glass fibers or other synthetic resins, so dismantling the finished product or sorting out impurities must be preceded. Resin waste should be additionally sorted according to raw materials.

본 발명은 회수되는 폐기되는 나일론 수지 및 나일론 섬유 제품을 수집하여 효율적으로 불순물을 제거하고 물성별로 분류한 후 특정한 색상과 물성을 보유한 나일론 재생 원료로 재가공하는 나일론 업싸이클 가공방법을 제공하는 것을 목적으로 한다.The present invention aims to provide a nylon upcycle processing method that collects recovered and discarded nylon resin and nylon fiber products, efficiently removes impurities, classifies them by physical properties, and then reprocesses them into nylon recycled raw materials with specific colors and properties. do.

상술한 기술적 과제를 해결하기 위한 나일론 업싸이클 가공방법은, 입고된 나일론 폐자재 벌크에서 특정 나일론을 선별하는 제1 단계; 선별된 나일론 폐자재 벌크의 샘플을 용융하여 점도를 테스트하는 제2 단계; 나일론 폐자재 벌크의 점도와 색상에 따라 분류하는 제3 단계; 다수의 나일론 폐자재 벌크를 원하는 점도와 색상에 따라 선택적으로 블렌딩하는 제 4단계; 및 블렌딩한 나일론 폐자재 벌크에 첨가제를 혼합하여 용융 가공하여 나일론 재생 원료를 생산하는 제5 단계;를 포함하는 것을 특징으로 한다.A nylon upcycle processing method for solving the above-described technical problem, a first step of selecting a specific nylon from the stocked nylon waste material bulk; a second step of melting a sample of the sorted nylon waste material bulk to test the viscosity; a third step of classifying the bulk nylon waste material according to viscosity and color; a fourth step of selectively blending a plurality of bulk nylon waste materials according to a desired viscosity and color; and a fifth step of mixing an additive with the blended bulk nylon waste material and melt-processing to produce a recycled nylon raw material.

이때, 상기 제1 단계는, 입고된 나일론 폐자재 벌크에서 불순물을 선별하여 제거하는 제1-1 단계; 및 불순물이 제거된 나일론 폐자재 벌크에서 나일론 6과 나일론 66을 선별하여 분류하는 제1-2 단계;를 포함하는 것을 특징으로 한다.In this case, the first step may include a step 1-1 of sorting and removing impurities from the stocked nylon waste material bulk; and a 1-2 step of sorting and sorting nylon 6 and nylon 66 from the bulk of the nylon waste material from which impurities have been removed.

또한, 상기 제1-1 단계는, 입고된 나일론 폐자재 벌크의 샘플을 일정 온도 이상으로 연소시킨 후 잔류량과 잔류율에 따라 불순물 함유 여부를 판단하는 애쉬 테스트 과정을 포함하는 것을 특징으로 한다.In addition, the step 1-1, after burning a sample of the stocked nylon waste material bulk above a certain temperature, characterized in that it includes an ash test process of determining whether impurities are contained according to the residual amount and residual rate.

또한, 상기 제1-2 단계는, 불순물이 제거된 나일론 폐자재 벌크의 샘플을 나일론 6의 용융점보다는 높으며 나일론 66의 용융점보다는 낮은 온도로 가열하여 나일론 6과 나일론 66의 혼재 여부를 판단하는 멜팅 테스트 과정을 포함하는 것을 특징으로 한다.In addition, in step 1-2, a melting test of determining whether nylon 6 and nylon 66 are mixed by heating a sample of a bulk nylon waste material from which impurities are removed to a temperature higher than the melting point of nylon 6 and lower than the melting point of nylon 66 It is characterized by including the process.

한편, 상기 첨가제는, 최종 산출물의 색상을 구현하기 위한 안료를 포함하는 것을 특징으로 한다.On the other hand, the additive is characterized in that it includes a pigment for realizing the color of the final product.

본 발명은 수집되어 회수되는 나일론 수지 및 나일론 섬유 제품 등 나일론 폐자재 벌크에서 샘플을 채취하여 불순물을 함유하는지 여부를 테스트한 후 불순물을 선별하는 작업을 수행하고, 나일론 6과 나일론 66 제품이 혼재하는지 여부를 테스트한 후 나일론 종류별로 분류하는 작업을 수행함으로써, 나일론 폐자재 벌크에서 불순물을 제거하고 종류별로 분류하는 작업에 최소한의 설비와 인원을 투입할 수 있다는 장점이 있다.The present invention collects and collects samples from bulk nylon waste materials such as nylon resin and nylon fiber products, which are collected and recovered, and tests whether they contain impurities, and then performs an operation to screen impurities, and whether nylon 6 and nylon 66 products are mixed. By performing the classification by type of nylon after testing whether or not there is, there is an advantage in that it is possible to remove impurities from the bulk of nylon waste material and put the minimum amount of equipment and personnel into the operation of sorting by type.

또한, 본 발명은 나일론 폐자재 벌크의 샘플에 대하여 점도 등 물성 테스트를 수행하여 점도와 색상에 따라 나일론 폐자재 벌크를 분류한 후, 다양한 점도나 색상의 나일론 폐자재 벌크들을 블렌딩하여 균일하고 우수한 점도와 색상을 가지는 나일론 재생 원료로 업싸이클 할 수 있다는 다른 장점이 있다.In addition, the present invention performs a physical property test such as viscosity on a sample of the nylon waste material bulk to classify the nylon waste material bulk according to the viscosity and color, and then blends the nylon waste material bulks of various viscosities or colors to achieve uniform and excellent viscosity Another advantage is that it can be upcycled to recycled nylon with color and color.

도 1은 본 발명의 일실시예에 따른 나일론 업싸이클 가공방법의 블록공정도이다.
도 2는 본 발명의 일실시예에 따른 나일론 폐자재 벌크의 샘플에 대하여 멜팅 테스트를 수행한 결과물의 사진이다.
도 3은 본 발명의 일실시예에 따른 나일론 업싸이클 가공방법을 거친 최종 나일론 재생 원료의 사진이다.
1 is a block process diagram of a nylon upcycle processing method according to an embodiment of the present invention.
2 is a photograph of a result of performing a melting test on a sample of a bulk nylon waste material according to an embodiment of the present invention.
3 is a photograph of the final recycled nylon raw material that has undergone the nylon upcycle processing method according to an embodiment of the present invention.

이하에서 개시되는 본 발명에 의한 실시예들은 본 발명의 특징과 효과, 그것들을 달성하기 위한 방법을 명확하게 하기 위한 목적으로 예시된 것으로서 특정한 실시 형태에 한정하려는 것이 아니며, 본 발명의 기술적 사상 및 범위에 포함되는 모든 변경, 균등물 또는 대체물을 포함하는 것으로 이해되어야 한다.The embodiments according to the present invention disclosed below are exemplified for the purpose of clarifying the characteristics and effects of the present invention, and a method for achieving them, and are not intended to be limited to specific embodiments, and the technical spirit and scope of the present invention It is to be understood as including all modifications, equivalents or substitutes included in

본 발명에 의한 실시예에서 "포함하다" 또는 "가지다" 등의 용어는 명세서 상에 기재된 특징, 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것이 존재함을 지정하려는 것이지, 하나 또는 그 이상의 다른 특징들이나 숫자, 단계, 동작, 구성요소, 부품 또는 이들을 조합한 것들의 존재 또는 부가 가능성을 미리 배제하지 않는 것으로 이해되어야 한다.In the embodiment according to the present invention, terms such as "comprises" or "have" are intended to designate that the features, numbers, steps, operations, components, parts, or combinations thereof described in the specification exist, and one or the It should be understood that the existence or addition of the above other features or numbers, steps, operations, components, parts or combinations thereof is not precluded in advance.

본 발명에 의한 실시예에서 사용되는 용어는 단지 특정한 실시예를 설명하기 위해 사용된 것으로서 본 발명에 의한 실시예를 한정하려는 의도가 아니며, 단수의 표현은 문맥상 명백하게 다르게 뜻하지 않는 한 복수의 표현을 포함한다.The terms used in the embodiments according to the present invention are only used to describe specific embodiments and are not intended to limit the embodiments according to the present invention, and the singular expression refers to a plural expression unless the context clearly indicates otherwise. include

본 발명에 의한 실시예에서 다르게 정의되지 않는 한, 기술적이거나 과학적인 용어를 포함하여 여기에서 사용되는 모든 용어는 본 발명이 속하는 기술분야에서 일반적인 지식을 가진 사람에 의해 일반적으로 이해되는 것과 동일한 의미를 가지고 있다.Unless otherwise defined in the embodiments of the present invention, all terms used herein, including technical or scientific terms, have the same meaning as commonly understood by a person of ordinary skill in the art to which the present invention belongs. Have.

일반적으로 사용되는 사전에 정의되어 있는 것과 같은 용어들은 관련 기술의 문맥 상 가지는 의미와 일치하는 의미를 가지는 것으로 해석되어야 하며, 본 발명에 의한 실시예에서 명백하게 정의되지 않는 한, 이상적이거나 과도하게 형식적인 의미로 해석되지 않는다.Terms such as those defined in a commonly used dictionary should be interpreted as having a meaning consistent with the meaning in the context of the related art, and unless explicitly defined in the embodiment of the present invention, ideal or excessively formal terms not interpreted as meaning

이하에서는 본 발명의 구체적인 실시예를 첨부된 도면을 참조하여 상세하게 설명하도록 한다.Hereinafter, specific embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도 1을 참조하면, 본 발명의 일실시예에 따른 나일론 업싸이클 가공방법은 입고되는 나일론 폐자재 벌크에서 샘플을 채취하여 나일론 폐자재 벌크에 유리섬유나 금속 등과 같은 불순물이 섞여 있는지 확인하는 단계로 시작된다. 나일론 폐자재 벌크에 불순물이 섞여 있는지는 일일이 육안으로 확인할 수도 있겠지만, 샘플을 채취하여 샘플에 대한 애쉬 테스트를 진행하여 불순물이 섞여 있는지, 어느 정도의 비율로 섞여 있는지 확인하는 것이 바람직할 것이다.Referring to Figure 1, the nylon upcycle processing method according to an embodiment of the present invention is a step of checking whether impurities such as glass fibers or metals are mixed in the nylon waste material bulk by collecting a sample from the received nylon waste material bulk. begins Although it is possible to visually check whether impurities are mixed in the bulk of the nylon waste material, it would be desirable to collect a sample and conduct an ash test on the sample to check whether impurities are mixed in and to what ratio.

애쉬 테스트는 샘플을 일정 온도 이상으로 가열하여 나일론 소재를 연소시킨 후 남은 잔류량에 따라 불순물 함유 여부를 확인하는 테스트이다. 아래 표 1은 특정 나일론 폐자재 벌크의 샘플에 대한 애쉬 테스트를 수행한 결과이다.The ash test is a test to check whether or not impurities are contained according to the residual amount after burning the nylon material by heating the sample to a certain temperature or more. Table 1 below shows the results of performing an ash test on a sample of a specific nylon waste material bulk.

테스트 전(무게, g)Before test (weight, g) 테스트 후(무게, g)After test (weight, g) 테스트 조건test requirements 도가니Crucible 투입시료input sample synthesis 도가니Crucible 잔류량residual amount 잔류율Retention rate 가열온도heating temperature 가열시간heating time 37.33937.339 3.0983.098 40.43740.437 37.34637.346 0.0070.007 0.23%0.23% 800℃800℃ 60분60 minutes

상기 표 1에 따르면 애쉬 테스트 결과, 애쉬 잔류량이 0.007g으로 잔류율은 0.23%으로 양호하였으며, 이에 따라 입고된 나일론 폐자재 벌크에는 불순물이 거의 섞여 있지 않은 것을 알 수 있으며, 별도의 불순물 제거 단계를 거치지 않고 다음 단계로 진행하게 된다.According to Table 1, as a result of the ash test, the residual amount of ash was 0.007 g and the residual rate was 0.23%, which was good. Accordingly, it can be seen that the bulk of the nylon waste material received was hardly mixed with impurities, and a separate impurity removal step was performed. It will proceed to the next step without going through it.

아래 표 2는 다른 특정 나일론 폐자재 벌크의 샘플에 대한 애쉬 테스트를 수행한 결과이다.Table 2 below shows the results of performing ash testing on samples of other specific bulk nylon waste materials.

테스트 전(무게, g)Before test (weight, g) 테스트 후(무게, g)After test (weight, g) 테스트 조건test requirements 도가니Crucible 투입시료input sample synthesis 도가니Crucible 잔류량residual amount 잔류율Retention rate 가열온도heating temperature 가열시간heating time 34.71934.719 3.0753.075 37.79437.794 34.92634.926 0.2070.207 6.73%6.73% 800℃800℃ 60분60 minutes

상기 표 2에 따르면 애쉬 테스트 결과, 애쉬 잔류량이 0.207g으로 잔유율은 6.73%를 기록하였는바, 입고된 나일론 폐자재 벌크에는 유리섬유나 금속 등과 같은 불순물이 다소 섞여 있을 가능성이 높으므로 별도의 불순물 제거 작업을 수행하도록 한다.According to Table 2, as a result of the ash test, the residual amount of ash was 0.207 g and the residual oil ratio was 6.73%. to perform the removal operation.

이와 같이 입고된 나일론 폐자재 벌크에 대한 불순물 함유 여부를 확인하고 불순물 제거 작업을 수행한 후, 나일론 폐자재 벌크에 나일론 6과 나일론 66이 혼재되어 있는지를 확인하는 작업을 수행한다.After confirming whether the bulk of the nylon waste material received in this way contains impurities and removing impurities, it is performed to check whether nylon 6 and nylon 66 are mixed in the bulk of the nylon waste material.

나일론 6과 나일론 66은 육안으로 구별하기 어려우므로 별도의 확인 작업이 필요하며, 본 발명의 일실시예에서는 나일론 6과 나일론 66의 용융점 차이를 이용한 멜팅 테스트를 통하여 판별하도록 하였다.Nylon 6 and nylon 66 are difficult to distinguish with the naked eye, so a separate confirmation operation is required.

즉, 입고된 나일론 폐자재 벌크의 샘플을 나일론 6의 용융점인 약 230℃ 보다는 높으며, 나일론 66의 용융점인 약 275℃보다는 낮은 온도로 가열하여 샘플의 용융 정도나 형태에 따라 나일론 6과 나일론 66이 혼재되어 있는지를 판별하도록 한다. That is, a sample of the stocked nylon waste material bulk is heated to a temperature higher than the melting point of nylon 6, about 230° C., and lower than the melting point of nylon 66, about 275° C. to determine if they are mixed.

도 2에는 이와 같이 멜팅 테스트를 수행한 결과물의 사진이 도시되어 있는데, 도 2(a)와 같이 샘플이 전체적으로 일정하게 용융되어 있는 경우에는 입고된 나일론 폐자재 벌크에 나일론 6만이 함유되어 있는 것으로 판별한다. 그러나, 도 2(b)와 같이 샘플이 일정하게 용융되어 있는 것이 아니라 용융되지 못한 덩어리가 섞여 있는 경우에는 입고된 나일론 폐자재 벌크에 나일론 6과 나일론 66이 혼재되어 있는 것으로 판별하도록 한다.FIG. 2 shows a photograph of the result of performing the melting test as described above. When the sample is uniformly melted as a whole as shown in FIG. 2(a), it is determined that only nylon 6 is contained in the stocked nylon waste material bulk. do. However, if the sample is not melted uniformly as shown in FIG. 2(b), but a lump that has not been melted is mixed, it is determined that nylon 6 and nylon 66 are mixed in the stocked nylon waste material bulk.

이와 같이 나일론 6과 나일론 66이 혼재되어 있는 나일론 폐자재 벌크는 별도의 선별 단계를 거쳐 나일론 6과 나일론 66의 혼입 생산을 방지하도록 하여야 한다. 이러한 선별 작업은 역시 나일론 6과 나일론 66의 용융점 차이를 이용하여 수행할 수 있을 것이다.As such, the bulk nylon waste material in which nylon 6 and nylon 66 are mixed must undergo a separate screening step to prevent mixed production of nylon 6 and nylon 66. This sorting operation could also be done using the difference in melting point between nylon 6 and nylon 66.

나일론 폐자재 벌크에 대한 불순물 제거와 종류별 선별 작업이 완료된 후에는 나일론 폐자재 벌크의 샘플에 대한 점도 테스트를 수행하도록 한다. 입고되는 다양한 나일론 폐자재 벌크는 다양한 점도를 가지고 있을 것인데, 이를 고려하지 않고 그대로 용융하여 최종 나일론 재생 원료로 가공하는 경우 물성이 균일하지 못하게 되어 품질에 문제가 발생할 것이다.After the removal of impurities and sorting by type of the nylon waste material bulk is completed, a viscosity test of the nylon waste material bulk sample should be performed. The various bulk of nylon waste material received will have various viscosities, and if it is melted without taking this into account and processed into the final nylon recycled raw material, the physical properties will not be uniform and quality problems will occur.

이를 방지하기 위하여, 입고되는 나일론 폐자재 벌크별로 점도를 테스트한 후 이를 분류한 후, 다수의 나일론 폐자재 벌크를 선택적으로 블렌딩하여 최종 나일론 재생 원료로 가공하여 물성이 균일하도록 하는 것이 바람직할 것이다.In order to prevent this, it would be desirable to test the viscosity for each incoming nylon waste material bulk and classify it, then selectively blend a number of nylon waste material bulks and process it into a final nylon recycled raw material so that the physical properties are uniform.

아래 표 3은 입고된 다수의 나이론 폐자재 벌크의 샘플들을 각각 용융하여 점도 테스트(Melt Index Test)를 수행한 결과이다.Table 3 below shows the results of performing a viscosity test (Melt Index Test) by melting each of a plurality of stocked nylon waste material bulk samples.

구분division 측정시간measurement time 시료무게sample weight MIMI 테스트 조건test requirements 설정온도set temperature 용융시간melting time 하중weight 샘플1sample 1 16.3016.30 2.112.11 77.777.7 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플2sample 2 21.0421.04 2.102.10 59.959.9 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플3sample 3 16.5616.56 2.112.11 76.476.4 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플4sample 4 16.9516.95 2.122.12 75.075.0 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플5sample 5 18.6218.62 2.112.11 68.068.0 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플6sample 6 17.3217.32 2.082.08 72.172.1 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플7sample 7 20.7420.74 2.052.05 59.359.3 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플8sample 8 18.2618.26 2.102.10 69.069.0 275℃275℃ 5′00″5′00″ 2.16kg2.16kg

상기 표 3에서 알 수 있듯이 입고되는 나일론 폐자재 벌크에 따라 어느 벌크는 높은 점도를 가지고 있고 어느 벌크는 낮은 점도를 가지고 있어, 균일한 물성을 보이지 못하고 있다.As can be seen from Table 3, some bulks have high viscosity and some bulk have low viscosity depending on the bulk of the nylon waste material to be stocked, and thus, uniform physical properties are not shown.

아래 표 4는 점도별로 분류된 나일론 폐자재 벌크들을 선택적으로 블렌딩한 후 각각의 샘플들을 추출하여 점도 테스트를 수행한 결과이다.Table 4 below shows the results of performing a viscosity test by selectively blending nylon waste material bulks classified by viscosity and then extracting each sample.

구분division 측정시간measurement time 시료무게sample weight MIMI 테스트 조건test requirements 설정온도set temperature 용융시간melting time 하중weight 샘플1sample 1 18.2818.28 2.092.09 68.668.6 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플2sample 2 18.2318.23 2.092.09 68.868.8 276℃276℃ 5′01″5′01″ 2.17kg2.17kg 샘플3sample 3 18.3518.35 2.072.07 67.767.7 275℃275℃ 5′00″5′00″ 2.16kg2.16kg 샘플4sample 4 18.1818.18 2.092.09 69.069.0 276℃276℃ 5′01″5′01″ 2.17kg2.17kg 샘플5sample 5 18.1018.10 2.092.09 69.369.3 277℃277℃ 5′02″5′02″ 2.18kg2.18kg 샘플6sample 6 18.1618.16 2.092.09 69.169.1 278℃278℃ 5′03″5′03″ 2.19kg2.19kg 샘플7sample 7 18.4318.43 2.072.07 67.467.4 279℃279℃ 5′04″5′04″ 2.20kg2.20kg 샘플8sample 8 18.4918.49 2.092.09 67.867.8 280℃280℃ 5′05″5′05″ 2.21kg2.21kg

상기 표 4에서 알 수 있듯이 나일론 폐자재 벌크를 선택적으로 블렌딩한 후에 각각의 샘플들은 균일한 점도를 나타내고 있다.As can be seen from Table 4 above, each sample exhibited a uniform viscosity after selectively blending the bulk nylon waste material.

한편, 입고된 나일론 폐자재 벌크의 점도에 따라 분류하는 것 외에도 색상에 따라 분류하는 것도 필요할 것이다. 이는 색상 별로 분류된 나일론 폐자재 벌크들을 선택적으로 블렌딩하여 특정 색상의 최종 나일론 재생 원료를 생산하기 위한 것이다. 만약, 나일론 폐자재 벌크들을 선택적으로 블렌딩하여도 특정 색상을 구현하기 어려운 경우에는 첨가제로써 특정 색상의 안료를 혼합하여 가공하도록 한다. 나일론 폐자제와 혼합되는 첨가제로는 안료 이외에도, 특정 성분의 오일이나 다른 합성수지 재료, 유리 섬유 등이 사용될 수가 있을 것이다.On the other hand, in addition to classification according to the viscosity of the received nylon waste bulk, it will also be necessary to classify according to color. This is to selectively blend color-sorted nylon waste bulks to produce a final recycled nylon material of a specific color. If it is difficult to realize a specific color even by selectively blending bulk nylon waste materials, a pigment of a specific color is mixed as an additive to be processed. As an additive to be mixed with the nylon waste material, in addition to the pigment, a specific component of oil, other synthetic resin materials, glass fibers, and the like may be used.

도 3에는 본 발명의 일실시예에 따른 나일론 업싸이클 가공방법을 거친 최종 나일론 재생 원료의 사진이다. 도 3에서 알 수 있듯이 본 발명에 의한 나일론 업싸이클 가공방법에 따라 나일론 폐자재 벌크에서 불순물을 제거하고 나일론 종류에 따라 선별하며, 점도와 색상 등에 따라 블렌딩하여 가공 성형한 경우 매우 균일한 품질의 최종 나일론 재생 원료를 획득할 수가 있다.3 is a photograph of the final recycled nylon raw material that has undergone the nylon upcycle processing method according to an embodiment of the present invention. As can be seen from Fig. 3, according to the nylon upcycle processing method according to the present invention, impurities are removed from the nylon waste material bulk, selected according to the nylon type, and blended according to viscosity and color, etc. Nylon recycled raw materials can be obtained.

이상에서 본 발명의 일실시예에 따른 나일론 업싸이클 가공방법을 살펴보았는데, 상술한 가공 단계 이외에 일반적으로 수행되는 나일론 폐자제에 대한 세척이나 건조 단계, 절단이나 파쇄 단계 등이 더 포함될 수 있음은 물론이다.In the above, the nylon upcycle processing method according to an embodiment of the present invention has been described. In addition to the above-described processing steps, washing or drying steps, cutting or crushing steps, etc. for the generally performed nylon waste material may be further included. to be.

이상에서 본 발명을 구체적인 실시예를 들어 상세하게 설명하였지만, 이는 본 발명의 바람직한 실시예를 예시적으로 설명한 것이지 본 발명을 한정한 것은 아니다. 따라서, 본 발명이 속하는 기술분야에서 일반적인 지식을 가진 사람이라면 본 발명의 기술적 사상의 범주를 벗어나지 않는 범위 내에서 여러가지 다양한 변형이 제공될 수 있다.In the above, the present invention has been described in detail with reference to specific examples, but the preferred embodiments of the present invention are exemplarily described, and the present invention is not limited thereto. Accordingly, a person having general knowledge in the technical field to which the present invention pertains may provide various modifications without departing from the scope of the technical spirit of the present invention.

Claims (5)

입고된 나일론 폐자재 벌크에서 특정 나일론을 선별하는 제1 단계;
선별된 나일론 폐자재 벌크의 샘플을 용융하여 점도를 테스트하는 제2 단계;
나일론 폐자재 벌크의 점도와 색상에 따라 분류하는 제3 단계;
다수의 나일론 폐자재 벌크를 원하는 점도와 색상에 따라 선택적으로 블렌딩하는 제 4단계; 및
블렌딩한 나일론 폐자재 벌크에 첨가제를 혼합하여 용융 가공하여 나일론 재생 원료를 생산하는 제5 단계;를 포함하되,
상기 제1 단계는,
입고된 나일론 폐자재 벌크에서 불순물을 선별하여 제거하는 제1-1 단계; 및
불순물이 제거된 나일론 폐자재 벌크에서 나일론 6과 나일론 66을 선별하여 분류하는 제1-2 단계;를 포함하며,
상기 제1-1 단계는,
입고된 나일론 폐자재 벌크의 샘플을 일정 온도 이상으로 연소시킨 후 잔류량과 잔류율에 따라 불순물 함유 여부를 판단하는 애쉬 테스트 과정을 포함하는 것을 특징으로 하는 나일론 업싸이클 가공방법.
A first step of selecting a specific nylon from the stocked nylon waste material bulk;
a second step of melting a sample of the sorted nylon waste material bulk to test the viscosity;
a third step of classifying the bulk nylon waste material according to viscosity and color;
a fourth step of selectively blending a plurality of bulk nylon waste materials according to a desired viscosity and color; and
A fifth step of producing a recycled nylon raw material by mixing an additive with the blended nylon waste bulk and melt processing;
The first step is
Step 1-1 of sorting and removing impurities from the stocked nylon waste bulk; and
Including; the first and second steps of sorting and sorting nylon 6 and nylon 66 from the bulk of the nylon waste material from which impurities have been removed;
In step 1-1,
A nylon upcycle processing method comprising an ash test process of determining whether impurities are contained according to the residual amount and residual rate after burning a sample of the stocked nylon waste material bulk over a certain temperature.
삭제delete 삭제delete 청구항 1에 있어서,
상기 제1-2 단계는,
불순물이 제거된 나일론 폐자재 벌크의 샘플을 나일론 6의 용융점보다는 높으며 나일론 66의 용융점보다는 낮은 온도로 가열하여 나일론 6과 나일론 66의 혼재 여부를 판단하는 멜팅 테스트 과정을 포함하는 것을 특징으로 하는 나일론 업싸이클 가공방법.
The method according to claim 1,
The first 1-2 steps,
Nylon up, characterized in that it includes a melting test process that determines whether nylon 6 and nylon 66 are mixed by heating a sample of a bulk nylon waste material from which impurities have been removed to a temperature higher than the melting point of nylon 6 and lower than the melting point of nylon 66 Cycle processing method.
청구항 1 또는 청구항 4에 있어서,
상기 첨가제는,
최종 산출물의 색상을 구현하기 위한 안료를 포함하는 것을 특징으로 하는 나일론 업싸이클 가공방법.
5. The method according to claim 1 or 4,
The additive is
Nylon upcycle processing method comprising a pigment for realizing the color of the final product.
KR1020210019191A 2021-02-10 2021-02-10 Processing Method For Nylon Upcycle KR102358506B1 (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20100005787A (en) * 2008-07-08 2010-01-18 주식회사에이엔에스 System for cutting and sorting spent fishing- nets
KR20100045695A (en) * 2008-10-24 2010-05-04 현대자동차주식회사 Recycling polyethyleneterephthalate composite and manufacturing method of thereof
KR101287121B1 (en) * 2013-05-31 2013-07-17 (주)남일엔프라 Processing method for cast nylon scrap

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20100005787A (en) * 2008-07-08 2010-01-18 주식회사에이엔에스 System for cutting and sorting spent fishing- nets
KR20100045695A (en) * 2008-10-24 2010-05-04 현대자동차주식회사 Recycling polyethyleneterephthalate composite and manufacturing method of thereof
KR101287121B1 (en) * 2013-05-31 2013-07-17 (주)남일엔프라 Processing method for cast nylon scrap

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